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Catalyst for preparing low carbon olefin by fixed bed, preparation method as well as use thereof

A technology of low-carbon olefins and catalysts, which is applied in the field of fixed-bed low-carbon olefin catalysts, preparation and application, which can solve the problems of low selectivity of low-carbon olefins, poor strength, poor thermal stability, low CO conversion rate, etc., to improve Reactivity, good thermal stability, and selectivity-enhancing effect

Active Publication Date: 2015-03-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is the problem of low CO conversion rate and low selectivity of low-carbon olefins in the product in the Fischer-Tropsch synthesis process of low-carbon olefins in the prior art, and the problem of poor strength and thermal stability of the catalyst under the conditions of use. Provide a new fixed-bed Fischer-Tropsch synthesis catalyst for producing low-carbon olefins, which has the advantages of high CO conversion rate and high selectivity of low-carbon olefins in the product when the catalyst is used for Fischer-Tropsch synthesis of low-carbon olefins

Method used

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  • Catalyst for preparing low carbon olefin by fixed bed, preparation method as well as use thereof
  • Catalyst for preparing low carbon olefin by fixed bed, preparation method as well as use thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Weigh 48.0 grams of ferric oxide (Fe 3 o 4 ), 15.0 grams of manganese oxide (MnO), 15.0 grams of copper oxide (CuO), 10.0 grams of potassium oxide (K 2 O), 7.0 grams of cerium oxide (CeO 2 ) and 5.0 g of antimony oxide (Sb 2 o 3 ) Six kinds of raw materials and 3 grams of carbon black powder with a weight percentage of 3% by weight of the total amount of raw materials were mixed in a ball mill for 2 hours; The kneaded material is kneaded until soft; the kneaded material is sent into the extruder, made into a strip with a diameter of 5mm, and cut into a column with a length of 20mm. After natural drying, it is sent to the drying equipment , dried at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace, calcined at 1200°C for 6.0 hours, and after cooling, crushed and sieved into 60-80 meshes to obtain the required fixed-bed Fischer-Tropsch synthesis system Low carbon olefin catalyst. The prepared catalyst comprises the following c...

Embodiment 2

[0031] Weigh 78.0 grams of ferric oxide (Fe 3 o 4 ), 6.0 grams of manganese oxide (MnO), 6.0 grams of copper oxide (CuO), 0.5 grams of potassium oxide (K 2 O), 0.5 g cerium oxide (CeO 2 ) and 9.0 g antimony oxide (Sb 2 o 3 ) Six kinds of raw materials and 3 grams of carbon black powder with a weight percentage of 3% by weight of the total amount of raw materials were mixed in a ball mill for 2 hours; The kneaded material is kneaded until soft; the kneaded material is sent into the extruder, made into a strip with a diameter of 5mm, and cut into a column with a length of 20mm. After natural drying, it is sent to the drying equipment , dried at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace, calcined at 1600°C for 2.0 hours, and after cooling, crushed and sieved into 60-80 meshes to obtain the required fixed-bed Fischer-Tropsch synthesis system Low carbon olefin catalyst. The prepared catalyst comprises the following components in ...

Embodiment 3

[0034] Weigh 19.0 grams of ferric oxide (Fe 3 o 4 ), 48.0 grams of manganese oxide (MnO), 8.0 grams of copper oxide (CuO), 24.3 grams of potassium oxide (K 2 O), 0.4 g cerium oxide (CeO 2 ) and 0.3 g antimony oxide (Sb 2 o 3 ) Six kinds of raw materials and 3 grams of carbon black powder with a weight percentage of 3% by weight of the total amount of raw materials were mixed in a ball mill for 2 hours; The kneaded material is kneaded until soft; the kneaded material is sent into the extruder, made into a strip with a diameter of 5mm, and cut into a column with a length of 20mm. After natural drying, it is sent to the drying equipment , dried at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace, calcined at 800°C for 10.0 hours, and after cooling, crushed and sieved into 60-80 meshes to obtain the required fixed-bed Fischer-Tropsch synthesis system Low carbon olefin catalyst. The prepared catalyst comprises the following components i...

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Abstract

The invention relates to a catalyst for preparing low carbon olefin by a fixed bed, a preparation method as well as use thereof, which mainly solves the problem that the CO conversion ratio is low and low carbon olefin selectivity is low in synthesis gas to low carbon reaction in the prior art and the catalyst is poor in intensity and thermal stability under a using condition. By adopting the technical scheme that the catalyst provided by the invention comprises the following components in parts by weight: a) 30-80 parts of iron element and oxides thereof; b) 10-40 parts of at least one element selected from manganese and chromium or oxides thereof; c) 10-40 parts of at least one element selected from copper and zinc or oxides thereof; d) 0.9-20 parts of at least one element selected from potassium and cesium or oxides thereof; e) 0.9-20 parts of at least one element selected from cerium and neodymium or oxides thereof; and f) 0.5-10 parts of an antimony element or oxides thereof, the problem is better solved, and the catalyst can be used for industrial production of Fischer-Tropsch synthesis to prepare low carbon olefin.

Description

technical field [0001] The invention relates to a fixed-bed low-carbon olefin catalyst, a preparation method and an application thereof. Background technique [0002] Low-carbon olefins refer to olefins with carbon atoms less than or equal to 4. Low-carbon olefins represented by ethylene and propylene are very important basic organic chemical raw materials. With the rapid growth of my country's economy, the supply of low-carbon olefins has been in short supply for a long time. At present, the production of low-carbon olefins mainly adopts the petrochemical route of cracking light hydrocarbons (ethane, naphtha, light diesel oil). Due to the increasing shortage of global oil resources and the long-term high price of crude oil, the development of low-carbon olefins industry only relies on oil The tubular cracking furnace process with light hydrocarbons as raw materials will encounter more and more raw material problems, and the production process and raw materials of low-carbo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/889C07C1/04C07C9/04C07C9/02C07C11/04C07C11/06C07C11/08
CPCY02P20/52
Inventor 李剑锋陶跃武宋卫林庞颖聪
Owner CHINA PETROLEUM & CHEM CORP
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